CA3159257C - Drying device and method for drying compressed gas - Google Patents
Drying device and method for drying compressed gas Download PDFInfo
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- CA3159257C CA3159257C CA3159257A CA3159257A CA3159257C CA 3159257 C CA3159257 C CA 3159257C CA 3159257 A CA3159257 A CA 3159257A CA 3159257 A CA3159257 A CA 3159257A CA 3159257 C CA3159257 C CA 3159257C
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- 238000001035 drying Methods 0.000 title claims abstract description 84
- 238000000034 method Methods 0.000 title claims abstract description 53
- 238000001816 cooling Methods 0.000 claims abstract description 112
- 239000012080 ambient air Substances 0.000 claims abstract description 31
- 239000002274 desiccant Substances 0.000 claims abstract description 19
- 230000001105 regulatory effect Effects 0.000 claims abstract description 15
- 238000007664 blowing Methods 0.000 claims abstract description 5
- 230000008929 regeneration Effects 0.000 claims description 37
- 238000011069 regeneration method Methods 0.000 claims description 37
- 238000010438 heat treatment Methods 0.000 claims description 8
- 239000007789 gas Substances 0.000 description 97
- 239000003570 air Substances 0.000 description 10
- 238000001179 sorption measurement Methods 0.000 description 5
- 239000006096 absorbing agent Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0438—Cooling or heating systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0446—Means for feeding or distributing gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0454—Controlling adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40003—Methods relating to valve switching
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40088—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
- B01D2259/4009—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating using hot gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/402—Further details for adsorption processes and devices using two beds
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Drying Of Gases (AREA)
- Drying Of Solid Materials (AREA)
Abstract
Method for drying compressed gas by means of a drying device with an inlet and an outlet comprising at least two vessels filled with a regenerable desiccant and a controllable valve system, consisting of a first and a second valve block connecting the inlet, respectively the outlet to the vessels, the valve system is being regulated as such that one vessel will dry compressed gas, while the other vessel is successively regenerated and cooled. The method comprises a first and a second cooling cycle, wherein the first cooling cycle consists of passing ambient air through the vessel to be cooled and the second cooling cycle consists of branching off, expanding and sending dried compressed gas through the outlet to be branched off and then blowing it off through the vessel to be cooled, using either the first or the second cooling cycle, or both, depending on predetermined conditions.
Description
DRYING DEVICE AND METHOD FOR DRYING COMPRESSED GAS.
[0001] The current invention relates to a method and drying device for drying 5 compressed gas.
[0001] The current invention relates to a method and drying device for drying 5 compressed gas.
[0002] More specifically, the invention is intended for drying devices fitted with an inlet for compressed gas to be dried and an outlet for dried compressed gas, wherein the drying device includes at least two vessels filled with a regenerable desiccant and a controllable valve system connecting the aforementioned inlet and outlet to the aforementioned vessels, wherein the controllable valve system is such that at least one vessel will dry compressed gas, while the other vessel is successively regenerated and cooled, wherein the vessels will each in turn be drying compressed gas by regulation of the 15 valve system.
[0003] Regenerable desiccant means a desiccant that can absorb moisture from a gas by adsorption and, when saturated with moisture, can be dried by transmitting a so-called regeneration gas through it. This process is also called 20 regeneration of the desiccant. The regeneration gas is typically a hot gas.
[0004] Although this is the principle of adsorption, the invention can also be applied to the principle of absorption.
25 [0005] When a vessel will dry, it will absorb moisture from the compressed gas to be dried, saturating the desiccant.
[0006] This vessel is then regenerated, typically allowing warm air to pass through it. This warm air will extract moisture from the desiccant and 30 regenerate it.
[0007] Before the vessel is used again to dry compressed gas, it will first be cooled.
[0008] Methods are already in place wherein part of the dried compressed gas
25 [0005] When a vessel will dry, it will absorb moisture from the compressed gas to be dried, saturating the desiccant.
[0006] This vessel is then regenerated, typically allowing warm air to pass through it. This warm air will extract moisture from the desiccant and 30 regenerate it.
[0007] Before the vessel is used again to dry compressed gas, it will first be cooled.
[0008] Methods are already in place wherein part of the dried compressed gas
5 is branched off and expanded at the outlet of the drying device. As a result, the gas will cool down and then pass through the vessel to cool it down.
[0009] Afterwards, the used gas is blown off., 10 [0010] This method has the disadvantage that one loses part of the compressed and dried air to be able to cool the vessel, which is obviously undesirable.
[0011] There are also methods in which ambient air is passed through the 15 vessel in question.
[0012] This can be sucked in, for example, by means of a blower or the like.
[0013] It is possible that the sucked in air is passed through the vessel a 20 number of times, passing each time through an air-to-air cooler to be cooled down.
[0014] A disadvantage of this is that it is never possible to cool below the ambient temperature. At high ambient temperatures, there is a risk that the 25 sucked in air will be insufficiently cooled, so that the temperature of the vessel will not drop sufficiently after cooling.
[0015] In addition, if the cooler fails, the sucked in air will not be cooled, which can also cause the temperature of the vessel to drop insufficiently.
[0016] As a result, the vessel will not be able to extract as much moisture from the gas to be dried during its next adsorption cycle.
[0009] Afterwards, the used gas is blown off., 10 [0010] This method has the disadvantage that one loses part of the compressed and dried air to be able to cool the vessel, which is obviously undesirable.
[0011] There are also methods in which ambient air is passed through the 15 vessel in question.
[0012] This can be sucked in, for example, by means of a blower or the like.
[0013] It is possible that the sucked in air is passed through the vessel a 20 number of times, passing each time through an air-to-air cooler to be cooled down.
[0014] A disadvantage of this is that it is never possible to cool below the ambient temperature. At high ambient temperatures, there is a risk that the 25 sucked in air will be insufficiently cooled, so that the temperature of the vessel will not drop sufficiently after cooling.
[0015] In addition, if the cooler fails, the sucked in air will not be cooled, which can also cause the temperature of the vessel to drop insufficiently.
[0016] As a result, the vessel will not be able to extract as much moisture from the gas to be dried during its next adsorption cycle.
6 PC T/1112020/062470 [0017] The remaining moisture in the compressed gas can cause problems for the final consumers.
5 [0018] Another disadvantage is that by using ambient air, moisture will also enter the vessel.
[0019] As a result, the dew point at the outlet of the drying device can become too high, which is obviously undesirable.
[0020] This invention aims at solving at least one of the aforementioned and other disadvantages.
[0021] To this end, the invention concerns a method for drying compressed gas 15 by means of a drying device with an inlet for compressed gas to be dried and an outlet for dried compressed gas, comprising at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block which connects the aforementioned inlet, respectively the outlet, to the aforementioned vessels, wherein the controllable valve system is being regulated as such that at least one vessel will dry compressed gas, while the other vessel is successively regenerated and cooled, wherein, by regulating the valve system, the vessels dry each in turn compressed gas, characterized in that the method consists of providing a first and a second cooling cycle to cool the vessel being cooled, with the first 25 cooling cycle consisting of sending ambient air through the vessel and the second cooling cycle consisting of drying, to branch off compressed gas at the aforementioned outlet, expand it and pass it through the vessel to be cooled, after which this gas is then blown off, applying the first or second cooling cycle, or both, depending on predetermined conditions.
[0022] An advantage of such a method is that one will always be able to cool with the first cooling cycle, which is the most energy efficient, but still, if necessary and by choosing the predetermined conditions appropriately, one will be able to apply the second cooling cycle which is much more robust and secure as a kind of 'fail-safe'.
5 [0023] In this way, the compressed gas is always properly dried, even if, for example, the ambient temperature becomes too high, and in addition, the second cooling cycle is only used under the conditions that it is necessary.
[0024] In a preferred embodiment, after the vessel being cooled with the first cooling cycle, the method consists of measuring or determining the temperature in this vessel or at the outlet of this vessel and, if this temperature is higher than a predetermined maximum temperature, additional cooling of this vessel with the second cooling cycle.
15 [0025] This has the advantage that always the most energy efficient first cooling cycle will be used to cool the vessel.
[0026] The second cooling cycle will only be used to further reduce the temperature of the vessel if necessary.
100271 In addition, when the second cooling cycle is switched on, this second cooling cycle will only have to perform a limited additional cooling, which means that it will have to be used for a shorter period of time.
25 [0028] In another preferred embodiment, the method includes the step of determining or measuring the dew point at the outlet or determining or measuring an average dew point at the outlet over a predetermined period of time prior to cooling the vessel being cooled, and:
30 - if this dew point is equal to or higher than a predetermined maximum dew point, cool this vessel with the second cooling cycle; and - if this dew point is lower than the predetermined maximum dew point, cool this vessel with the first cooling cycle.
[0029] In this case, if the dew point is too high, only the second cooling cycle 5 will be applied. Dry air is used for the second cooling cycle, so that moisture can also be extracted from the vessel in question during the cooling process.
[NM In this way, the vessel will be dried at the same time and additionally regenerated.
[0031/ It is important to note that the dew point is thus determined or measured when the vessel in question is in the adsorption phase, i.e. the dew point is determined or measured when the vessel in question is drying gas.
15 [0032] It is also possible to measure or determine the dew point during all or part of the adsorption phase and then take an average of it.
[0033] The invention also concerns a drying device which will allow the aforementioned method to be applied, i.e. to be able to apply both the first and 20 second cooling cycles.
[0034] To this end, the invention has as object a drying device for drying compressed gas, which drying device is equipped with an inlet for compressed gas to be dried and an outlet for dried compressed gas, wherein the drying 25 device includes at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block which connects the aforementioned inlet, respectively the aforementioned outlet, to the aforementioned vessels, wherein the valve system is being regulated as such that at least one vessel will dry compressed 30 gas, while the other vessel is successively regenerated and cooled, the vessels drying each in turn the compressed gases being controlled by the valve system, characterized in that the drying device is further equipped with a blower to suck in ambient air, a gas release port and a four-way valve that will allow either the blower or the gas release port to be connected to the vessels via the "first" valve block in such a way that, when the four-way valve connects the blower to the "first" valve block, the ambient air sucked in by the 5 blower can enter the vessel being cooled via the four-way valve and the "first"
valve block, in which the drying device is further equipped with a branch pipe capable of branching off dried compressed gas, expanding it and leading it through the 'second' valve block to the vessel being cooled in such a way that, when the four-way valve connects the gas release port with the 'first' valve 10 block, the branched gas can, after passing through the vessel being cooled, be discharged through the gas release port.
[0035] An advantage of such a drying device is that it will allow the use of a method according to the invention, i.e. to apply both the first cooling cycle and 15 the second cooling cycle.
[0036] By cleverly controlling the components of the drying device, in particular the four-way valve and the valve system, all necessary circuits can be created in a relatively compact way.
[0037] It goes without saying that all the aforementioned advantages of the method can also be applied to the device.
[0038] To better demonstrate the characteristics of the invention, the following 25 describes, by way of example without any restrictive character, a number of preferred embodiments of a method and a drying device in accordance with the invention, with reference to the accompanying drawings, in which:
figure 1 schematically shows a drying device in accordance with the invention;
30 figure 2 schematically shows the drying device in figure 1, but in a different position.
[0039] The drying device 1 schematically shown in figure 1 according to the invention for drying compressed gas consists essentially of two vessels 2 filled with a moisture absorber 3.
5 [0040] This regenerable moisture absorber 3 is also called desiccant.
[0041] It is of course possible that there are more than two vessels 2.
[0042] The drying device 1 further comprises a valve system 4 consisting of a 10 first valve block 5 and a second valve block 6.
[0043] The first valve block 5 will connect vessels 2 to an inlet 7 for dried compressed gas, while the second valve block 6 will connect vessels 2 to an outlet 8 for dried compressed gas.
[0044] The aforementioned valve blocks 5, 6 are a system of different pipes and valves which can be regulated in such a way that at any one time at least one vessel 21s being regenerated, while the other vessel 2 or the other vessels 2 are drying the compressed gas, wherein by regulating the valve system 4 20 the vessels 2 will each in turn dry compressed gas.
[0045] Furthermore, according to the invention, the drying device 1 is equipped with a four-way valve 9, a blower 10 for the intake of ambient air and a gas release port 11 for the release of gas, which are configured in such a way that 25 in a first position of the four-way valve 9 the blower 10 is connected to the vessels 2 via the first valve block 5, as shown in figure 1, and in a second position of the four-way valve 9 the gas release port 11 is connected to the vessels 2 via the first valve block 5, as shown in figure 2.
30 [0046] Of course, it is not excluded that instead of a blower 10, other means are provided for the intake of ambient air.
5 [0018] Another disadvantage is that by using ambient air, moisture will also enter the vessel.
[0019] As a result, the dew point at the outlet of the drying device can become too high, which is obviously undesirable.
[0020] This invention aims at solving at least one of the aforementioned and other disadvantages.
[0021] To this end, the invention concerns a method for drying compressed gas 15 by means of a drying device with an inlet for compressed gas to be dried and an outlet for dried compressed gas, comprising at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block which connects the aforementioned inlet, respectively the outlet, to the aforementioned vessels, wherein the controllable valve system is being regulated as such that at least one vessel will dry compressed gas, while the other vessel is successively regenerated and cooled, wherein, by regulating the valve system, the vessels dry each in turn compressed gas, characterized in that the method consists of providing a first and a second cooling cycle to cool the vessel being cooled, with the first 25 cooling cycle consisting of sending ambient air through the vessel and the second cooling cycle consisting of drying, to branch off compressed gas at the aforementioned outlet, expand it and pass it through the vessel to be cooled, after which this gas is then blown off, applying the first or second cooling cycle, or both, depending on predetermined conditions.
[0022] An advantage of such a method is that one will always be able to cool with the first cooling cycle, which is the most energy efficient, but still, if necessary and by choosing the predetermined conditions appropriately, one will be able to apply the second cooling cycle which is much more robust and secure as a kind of 'fail-safe'.
5 [0023] In this way, the compressed gas is always properly dried, even if, for example, the ambient temperature becomes too high, and in addition, the second cooling cycle is only used under the conditions that it is necessary.
[0024] In a preferred embodiment, after the vessel being cooled with the first cooling cycle, the method consists of measuring or determining the temperature in this vessel or at the outlet of this vessel and, if this temperature is higher than a predetermined maximum temperature, additional cooling of this vessel with the second cooling cycle.
15 [0025] This has the advantage that always the most energy efficient first cooling cycle will be used to cool the vessel.
[0026] The second cooling cycle will only be used to further reduce the temperature of the vessel if necessary.
100271 In addition, when the second cooling cycle is switched on, this second cooling cycle will only have to perform a limited additional cooling, which means that it will have to be used for a shorter period of time.
25 [0028] In another preferred embodiment, the method includes the step of determining or measuring the dew point at the outlet or determining or measuring an average dew point at the outlet over a predetermined period of time prior to cooling the vessel being cooled, and:
30 - if this dew point is equal to or higher than a predetermined maximum dew point, cool this vessel with the second cooling cycle; and - if this dew point is lower than the predetermined maximum dew point, cool this vessel with the first cooling cycle.
[0029] In this case, if the dew point is too high, only the second cooling cycle 5 will be applied. Dry air is used for the second cooling cycle, so that moisture can also be extracted from the vessel in question during the cooling process.
[NM In this way, the vessel will be dried at the same time and additionally regenerated.
[0031/ It is important to note that the dew point is thus determined or measured when the vessel in question is in the adsorption phase, i.e. the dew point is determined or measured when the vessel in question is drying gas.
15 [0032] It is also possible to measure or determine the dew point during all or part of the adsorption phase and then take an average of it.
[0033] The invention also concerns a drying device which will allow the aforementioned method to be applied, i.e. to be able to apply both the first and 20 second cooling cycles.
[0034] To this end, the invention has as object a drying device for drying compressed gas, which drying device is equipped with an inlet for compressed gas to be dried and an outlet for dried compressed gas, wherein the drying 25 device includes at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block which connects the aforementioned inlet, respectively the aforementioned outlet, to the aforementioned vessels, wherein the valve system is being regulated as such that at least one vessel will dry compressed 30 gas, while the other vessel is successively regenerated and cooled, the vessels drying each in turn the compressed gases being controlled by the valve system, characterized in that the drying device is further equipped with a blower to suck in ambient air, a gas release port and a four-way valve that will allow either the blower or the gas release port to be connected to the vessels via the "first" valve block in such a way that, when the four-way valve connects the blower to the "first" valve block, the ambient air sucked in by the 5 blower can enter the vessel being cooled via the four-way valve and the "first"
valve block, in which the drying device is further equipped with a branch pipe capable of branching off dried compressed gas, expanding it and leading it through the 'second' valve block to the vessel being cooled in such a way that, when the four-way valve connects the gas release port with the 'first' valve 10 block, the branched gas can, after passing through the vessel being cooled, be discharged through the gas release port.
[0035] An advantage of such a drying device is that it will allow the use of a method according to the invention, i.e. to apply both the first cooling cycle and 15 the second cooling cycle.
[0036] By cleverly controlling the components of the drying device, in particular the four-way valve and the valve system, all necessary circuits can be created in a relatively compact way.
[0037] It goes without saying that all the aforementioned advantages of the method can also be applied to the device.
[0038] To better demonstrate the characteristics of the invention, the following 25 describes, by way of example without any restrictive character, a number of preferred embodiments of a method and a drying device in accordance with the invention, with reference to the accompanying drawings, in which:
figure 1 schematically shows a drying device in accordance with the invention;
30 figure 2 schematically shows the drying device in figure 1, but in a different position.
[0039] The drying device 1 schematically shown in figure 1 according to the invention for drying compressed gas consists essentially of two vessels 2 filled with a moisture absorber 3.
5 [0040] This regenerable moisture absorber 3 is also called desiccant.
[0041] It is of course possible that there are more than two vessels 2.
[0042] The drying device 1 further comprises a valve system 4 consisting of a 10 first valve block 5 and a second valve block 6.
[0043] The first valve block 5 will connect vessels 2 to an inlet 7 for dried compressed gas, while the second valve block 6 will connect vessels 2 to an outlet 8 for dried compressed gas.
[0044] The aforementioned valve blocks 5, 6 are a system of different pipes and valves which can be regulated in such a way that at any one time at least one vessel 21s being regenerated, while the other vessel 2 or the other vessels 2 are drying the compressed gas, wherein by regulating the valve system 4 20 the vessels 2 will each in turn dry compressed gas.
[0045] Furthermore, according to the invention, the drying device 1 is equipped with a four-way valve 9, a blower 10 for the intake of ambient air and a gas release port 11 for the release of gas, which are configured in such a way that 25 in a first position of the four-way valve 9 the blower 10 is connected to the vessels 2 via the first valve block 5, as shown in figure 1, and in a second position of the four-way valve 9 the gas release port 11 is connected to the vessels 2 via the first valve block 5, as shown in figure 2.
30 [0046] Of course, it is not excluded that instead of a blower 10, other means are provided for the intake of ambient air.
7 [0047] It is also possible that instead of a four-way valve 9, a valve block with, for example, four valves or air inlets or other means can be used that can achieve the same configuration as the four-way valve 9.
5 [0048] As shown in figure 1, the drying device 1 is such that in the first position of the four-way valve 9, the ambient air sucked in by the blower 10 through the four-way valve 9 and the first valve block 5 can enter the vessel 2 which is being cooled.
10 [0049] Of course, the valve block 5 is regulated in the appropriate way to enable the right flow path for the gas.
[0050] In addition, the drying device 1 is equipped with a branch pipe 12 which can branch off dried compressed gas, expand it and lead it via the second 15 valve block 6 to the vessel 2 which is being cooled.
[0051] In this case, the aforementioned branch pipe 12 contains an expansion valve 13 to expand the branched dried compressed gas.
20 [0052] The aforementioned branch pipe 12 is preferably at least partially integrated in, or at least part of, the second valve block 6.
[0053] In this case, the branch pipe 12 is fully integrated in the second valve block 6.
[0054] As shown in figure 2, the drying device 1 is such that, when the four-way valve 9 is in the second position, the branched off gas can be blown off through the gas release port 11 after passing through the vessel 2 which is cooled.
[0055] Of course, the valve block 6 is regulated in the appropriate way to enable the right flow path for the gas.
5 [0048] As shown in figure 1, the drying device 1 is such that in the first position of the four-way valve 9, the ambient air sucked in by the blower 10 through the four-way valve 9 and the first valve block 5 can enter the vessel 2 which is being cooled.
10 [0049] Of course, the valve block 5 is regulated in the appropriate way to enable the right flow path for the gas.
[0050] In addition, the drying device 1 is equipped with a branch pipe 12 which can branch off dried compressed gas, expand it and lead it via the second 15 valve block 6 to the vessel 2 which is being cooled.
[0051] In this case, the aforementioned branch pipe 12 contains an expansion valve 13 to expand the branched dried compressed gas.
20 [0052] The aforementioned branch pipe 12 is preferably at least partially integrated in, or at least part of, the second valve block 6.
[0053] In this case, the branch pipe 12 is fully integrated in the second valve block 6.
[0054] As shown in figure 2, the drying device 1 is such that, when the four-way valve 9 is in the second position, the branched off gas can be blown off through the gas release port 11 after passing through the vessel 2 which is cooled.
[0055] Of course, the valve block 6 is regulated in the appropriate way to enable the right flow path for the gas.
8 [0056] In other words, an open cooling circuit 14 is formed, consisting of the branch pipe 12, the second valve block 6, the vessel 2 being cooled, the first valve block 5, the four-way valve 9 and the gas release port 11. This 5 aforementioned open cooling circuit 14 will be used for the second cooling cycle, as explained below.
[0057] In the example shown in figures 1 and 2, but not necessary for the invention, the drying device 1 is equipped with a cooling pipe 15 connecting 10 the second valve block 6 to the inlet side 16 of the blower 10.
[0058] From the figures it can be seen that a closed cooling circuit 17 will be formed when the four-way valve 9 is in the aforementioned first position, which is formed successively by the blower 10, the four-way valve 9, the first valve 16 block 5, a vessel 2, the second valve block 6 and the cooling pipe 15.
[0059] As can be seen in the figures, the cooling pipe 15 contains a cooler 18.
This cooler 18 can be, for example, an air-to-air cooler 18.
20 [0060] The aforementioned closed cooling circuit 17 will be used for the first cooling cycle, as explained below.
[0061] However, it is also possible for the invention to use an open circuit for the first cooling cycle. In this case, the aforementioned cooling pipe 15 with 25 cooler 18 will be absent, but will be replaced by a gas release port, release valve or similar connected to the second valve block 6. The open circuit for the first cooling cycle then consists of the blower 10, the four-way valve 9, the first valve block 5, a vessel 2, the second valve block 6 and the gas release port or release valve.
[0062] In addition, the drying device 1 is equipped with a regeneration pipe which connects the four-way valve 9 to the second valve block 6.
[0057] In the example shown in figures 1 and 2, but not necessary for the invention, the drying device 1 is equipped with a cooling pipe 15 connecting 10 the second valve block 6 to the inlet side 16 of the blower 10.
[0058] From the figures it can be seen that a closed cooling circuit 17 will be formed when the four-way valve 9 is in the aforementioned first position, which is formed successively by the blower 10, the four-way valve 9, the first valve 16 block 5, a vessel 2, the second valve block 6 and the cooling pipe 15.
[0059] As can be seen in the figures, the cooling pipe 15 contains a cooler 18.
This cooler 18 can be, for example, an air-to-air cooler 18.
20 [0060] The aforementioned closed cooling circuit 17 will be used for the first cooling cycle, as explained below.
[0061] However, it is also possible for the invention to use an open circuit for the first cooling cycle. In this case, the aforementioned cooling pipe 15 with 25 cooler 18 will be absent, but will be replaced by a gas release port, release valve or similar connected to the second valve block 6. The open circuit for the first cooling cycle then consists of the blower 10, the four-way valve 9, the first valve block 5, a vessel 2, the second valve block 6 and the gas release port or release valve.
[0062] In addition, the drying device 1 is equipped with a regeneration pipe which connects the four-way valve 9 to the second valve block 6.
9 [0063] In the second position of the four-way valve 9, when the four-way valve 9 connects gas release port 11 to the first valve block 5, the four-way valve will connect the blower 10 to the regeneration pipe 19 and thus to the second 5 valve block 6.
[0064] This regeneration pipe 19 is equipped with a heater 20, in this case an electric heater 20.
[0064] This regeneration pipe 19 is equipped with a heater 20, in this case an electric heater 20.
10 100651As can be seen from figure 2, in the second position of the four-way valve 9, a regeneration circuit 21 is formed comprising the blower 10, the four-way valve 9, the regeneration pipe 19 with the heater 20, the second valve block 6, the vessel 2 being regenerated, the first valve block 5, the four-way valve 9 and the gas release port 11.
[0066] In the second position of the four-way valve 9 a regeneration circuit is formed as well as the open cooling circuit 14 that is used for the second cooling cycle. The regeneration circuit 21, or the open cooling circuit 14, will be realized by an appropriate regulation of the valve blocks 5, 6.
[0067] As can be seen in the figures, in this case the regeneration pipe 19 and the cooling pipe 15 partially coincide.
[0068] In this case, only one pipe 22 will leave from the second valve block 6, 25 which also includes the aforementioned heating 20. The aforementioned pipe 22 splits into two separate pipes 22a, 22b, one of which leads to the inlet side 16 of the blower 10, in which the cooler 18 is included, and one to the four-way valve 9_ 30 [0069] It goes without saying that, in addition to the appropriate regulation of valve blocks 5, 6 and the four-way valve 9, the aforementioned heating 20 and cooler 18 are also appropriately controlled when implementing the open cooling circuit 14, the closed cooling circuit 17 and the regeneration circuit 21.
[0070] Finally, the drying device 1 in this case, but not necessary for the 6 invention, includes a temperature sensor 23 which can measure the temperature of the vessels 2 and a dew point sensor 24 which can measure the dew point at the outlet of the vessels 2. Both sensors 23, 24 in this case are located at the outlet side of the vessels 2, i.e. the side of the vessels connected to the outlet 8 of the drying device 1.
[0071] The operation of the drying device 1 and the method according to the invention for drying compressed gas using the drying device 1 is very simple and as follows.
[0072] During the operation of the drying device 1, compressed gas to be dried will enter the vessel 2 which is drying through the inlet 7_ [0073] When passing through this vessel 2, the desiccant 3 will extract moisture from the gas.
[0074] The dried compressed gas will leave the drying device 1 through the outlet 8.
[0075] The other vessel 2, which has already dried gas during a previous cycle.
contains moisture and is regenerated in the meantime.
[0076] A regeneration cycle is used, which consists of heating ambient air and sending it through the relevant vessel 2 and then blowing it off.
[0077] For this regeneration cycle, the aforementioned regeneration circuit 21 is used.
[0066] In the second position of the four-way valve 9 a regeneration circuit is formed as well as the open cooling circuit 14 that is used for the second cooling cycle. The regeneration circuit 21, or the open cooling circuit 14, will be realized by an appropriate regulation of the valve blocks 5, 6.
[0067] As can be seen in the figures, in this case the regeneration pipe 19 and the cooling pipe 15 partially coincide.
[0068] In this case, only one pipe 22 will leave from the second valve block 6, 25 which also includes the aforementioned heating 20. The aforementioned pipe 22 splits into two separate pipes 22a, 22b, one of which leads to the inlet side 16 of the blower 10, in which the cooler 18 is included, and one to the four-way valve 9_ 30 [0069] It goes without saying that, in addition to the appropriate regulation of valve blocks 5, 6 and the four-way valve 9, the aforementioned heating 20 and cooler 18 are also appropriately controlled when implementing the open cooling circuit 14, the closed cooling circuit 17 and the regeneration circuit 21.
[0070] Finally, the drying device 1 in this case, but not necessary for the 6 invention, includes a temperature sensor 23 which can measure the temperature of the vessels 2 and a dew point sensor 24 which can measure the dew point at the outlet of the vessels 2. Both sensors 23, 24 in this case are located at the outlet side of the vessels 2, i.e. the side of the vessels connected to the outlet 8 of the drying device 1.
[0071] The operation of the drying device 1 and the method according to the invention for drying compressed gas using the drying device 1 is very simple and as follows.
[0072] During the operation of the drying device 1, compressed gas to be dried will enter the vessel 2 which is drying through the inlet 7_ [0073] When passing through this vessel 2, the desiccant 3 will extract moisture from the gas.
[0074] The dried compressed gas will leave the drying device 1 through the outlet 8.
[0075] The other vessel 2, which has already dried gas during a previous cycle.
contains moisture and is regenerated in the meantime.
[0076] A regeneration cycle is used, which consists of heating ambient air and sending it through the relevant vessel 2 and then blowing it off.
[0077] For this regeneration cycle, the aforementioned regeneration circuit 21 is used.
11 [0078] For this purpose, the four-way valve 9 is placed in the second position and valve blocks 5, 6 are regulated in such a way that the regeneration circuit 21 is realized. In this case, the heating 20 is also switched on.
5 [0079] The blower 10 will suck in ambient air which passes through the regeneration pipe 19 along the heater 20 where the gas is heated.
[0080] Via the second valve block 6, the heated gas will be brought to the aforementioned other vessel 2, wherein it will draw moisture from the desiccant 10 when passing through this vessel 2.
[0081] Via the first valve block 5, the hot, moist gas will leave the drying device 1 through the gas release port II.
15 [0082] After the regeneration cycle, the heating 20 will be switched off_ [0083] When the desiccant 3 is regenerated, the vessel 2 will be cooled.
[0084] To this end, the method is applied according to the invention, which 20 essentially consists of providing a first cooling cycle and a second cooling cycle.
[0085] For the first cooling cycle the closed cooling circuit 17 is used, wherein ambient air is sent through the vessel 2 that is being cooled.
[0086] For the second cooling cycle, the open cooling circuit 14 is used, wherein dried compressed gas at the outlet 8 is branched off, expanded and passed through the vessel 2 that is being cooled, after which this gas is blown off.
[0087] The method consists of applying either the first or the second cooling cycle, or both, on the basis of predetermined conditions.
5 [0079] The blower 10 will suck in ambient air which passes through the regeneration pipe 19 along the heater 20 where the gas is heated.
[0080] Via the second valve block 6, the heated gas will be brought to the aforementioned other vessel 2, wherein it will draw moisture from the desiccant 10 when passing through this vessel 2.
[0081] Via the first valve block 5, the hot, moist gas will leave the drying device 1 through the gas release port II.
15 [0082] After the regeneration cycle, the heating 20 will be switched off_ [0083] When the desiccant 3 is regenerated, the vessel 2 will be cooled.
[0084] To this end, the method is applied according to the invention, which 20 essentially consists of providing a first cooling cycle and a second cooling cycle.
[0085] For the first cooling cycle the closed cooling circuit 17 is used, wherein ambient air is sent through the vessel 2 that is being cooled.
[0086] For the second cooling cycle, the open cooling circuit 14 is used, wherein dried compressed gas at the outlet 8 is branched off, expanded and passed through the vessel 2 that is being cooled, after which this gas is blown off.
[0087] The method consists of applying either the first or the second cooling cycle, or both, on the basis of predetermined conditions.
12 [0088] In a first alternative embodiment of the method, the method consists of cooling the vessel 2 in question with the first cooling cycle, using the closed cooling circuit 17 and the cooler 18.
[0089] The ambient air sucked in by the blower 10 will be circulated through the closed cooling circuit 17, after passing through the vessel 2, it will be cooled by the cooler 18. This cooled gas will then again be passed through the vessel 2 via the blower 10.
[0090] After the vessel 2 has been cooled with the first cooling cycle, the temperature of the vessel 2 is measured using the temperature sensor 23 provided for this purpose.
[0091] If this temperature is higher than a predetermined maximum temperature Tmax, this vessel 2 will be additionally cooled with the second cooling cycle.
[0092] The four-way valve 9 will then be switched to the position shown in figure 2, after which the second cooling cycle can be started, using the open cooling circuit 14 to cool the vessel 2 additionally, using the expanded and thus cooled dried compressed gas.
[0093] In order to expand the branched, dried compressed gas, the expansion valve 13 is used.
[0094] In a second alternative embodiment of the method, the method consists of determining or measuring the dew point at the outlet 8 using the dew point sensor 24 provided for this purpose before the vessel concerned is cooled 2.
[0095] If the dew point is lower than a predetermined maximum dew point DP, the vessel 2 will be cooled with the first cooling cycle.
[0089] The ambient air sucked in by the blower 10 will be circulated through the closed cooling circuit 17, after passing through the vessel 2, it will be cooled by the cooler 18. This cooled gas will then again be passed through the vessel 2 via the blower 10.
[0090] After the vessel 2 has been cooled with the first cooling cycle, the temperature of the vessel 2 is measured using the temperature sensor 23 provided for this purpose.
[0091] If this temperature is higher than a predetermined maximum temperature Tmax, this vessel 2 will be additionally cooled with the second cooling cycle.
[0092] The four-way valve 9 will then be switched to the position shown in figure 2, after which the second cooling cycle can be started, using the open cooling circuit 14 to cool the vessel 2 additionally, using the expanded and thus cooled dried compressed gas.
[0093] In order to expand the branched, dried compressed gas, the expansion valve 13 is used.
[0094] In a second alternative embodiment of the method, the method consists of determining or measuring the dew point at the outlet 8 using the dew point sensor 24 provided for this purpose before the vessel concerned is cooled 2.
[0095] If the dew point is lower than a predetermined maximum dew point DP, the vessel 2 will be cooled with the first cooling cycle.
13 [0096] However, if the dew point is equal to or higher than the predetermined maximum dew point DPrnax, the vessel 2 will be cooled with the second cooling cycle.
[0097] As mentioned above, during this second cooling cycle an additional drying of the desiccant 3 will take place in the vessel 2, causing the dew point to drop.
[0098] After completing the cooling of the vessel 2, this vessel 2 can be used to dry compressed gas, while the other vessel 2, previously used for drying, can now be regenerated and cooled in accordance with the aforementioned method.
[0099] Although in the aforementioned example of the method, for the first cooling cycle a closed cooling circuit 17 is used, after the ambient air is sucked in by means of a blower 10 or similar and the ambient air then circulates in the closed cooling circuit 17, it is not excluded that a non-closed circuit is used in which the sucked in ambient air is blown off after passing through the vessel that is being cooled.
[0100] This has the advantage that no cooler 18 is needed.
[0101] A disadvantage is that new ambient air is sucked in all the time to cool vessel 2.
[0102] As a result, if the ambient air is very moist, it is possible that too much moisture enters the vessel 2, which can cause the dew point at outlet 8 to rise too much.
[0097] As mentioned above, during this second cooling cycle an additional drying of the desiccant 3 will take place in the vessel 2, causing the dew point to drop.
[0098] After completing the cooling of the vessel 2, this vessel 2 can be used to dry compressed gas, while the other vessel 2, previously used for drying, can now be regenerated and cooled in accordance with the aforementioned method.
[0099] Although in the aforementioned example of the method, for the first cooling cycle a closed cooling circuit 17 is used, after the ambient air is sucked in by means of a blower 10 or similar and the ambient air then circulates in the closed cooling circuit 17, it is not excluded that a non-closed circuit is used in which the sucked in ambient air is blown off after passing through the vessel that is being cooled.
[0100] This has the advantage that no cooler 18 is needed.
[0101] A disadvantage is that new ambient air is sucked in all the time to cool vessel 2.
[0102] As a result, if the ambient air is very moist, it is possible that too much moisture enters the vessel 2, which can cause the dew point at outlet 8 to rise too much.
14 [0103] In this case, the aforementioned second alternative embodiment of the invention will be very advantageous, as it will allow the dew point to be lowered if necessary.
[0104] Another aspect of the invention concerns a method for drying compressed gas by means of a drying device with an inlet for the compressed gas to be dried and an outlet for the dried compressed gas, comprising at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block connecting the aforementioned inlet, respectively outlet to the aforementioned vessels, wherein the controllable valve system is being regulated as such that at least one vessel will dry compressed gas, while the other vessel is successively regenerated and cooled, wherein by regulating the valve system the vessels dry each in turn compressed gas, characterized in that the method consists of providing a regeneration cycle to regenerate a vessel which is being regenerated, wherein this regeneration cycle consists of heating ambient air, passing it through the vessel concerned and then blowing it off.
[0105] This means applying the aforementioned regeneration cycle in a known drying device 1, i.e. without necessarily having to apply the first and second cooling cycles.
[0106] The present invention is by no means limited to the embodiments described as examples and shown in the figures, but a method and device according to the invention can be implemented in all shapes and sizes without going beyond the scope of the invention.
[0107] The following aspects are also disclosed herein:
1.- A method for drying compressed gas by means of a drying device with an inlet for compressed gas to be dried and an outlet for dried compressed gas, which drying device comprises at least two vessels filled with a Date Recue/Date Received 2023-08-11 regenerable desiccant and a controllable valve system, consisting of a first valve block and a second valve block connecting the above inlet, respectively outlet to the aforementioned vessels, the controllable valve system being regulated such that at least one vessel will dry compressed gas, while the other vessel will be regenerated and cooled successively, wherein, by regulating the valve system, the vessels each, in turn, dry compressed gas, whereby the method consists of providing a first cooling cycle and a second cooling cycle to cool the vessel being cooled, wherein the first cooling cycle consists of passing ambient air through the vessel and the second cooling cycle consisting of branching off dried compressed gas at the aforementioned outlet, expand it and pass it through the vessel to be cooled, after which this gas is then blown off, wherein depending on predetermined conditions, the first cooling cycle or the second cooling cycle, or both, will be applied, wherein the method also consists, for the first cooling cycle, of using a closed cooling circuit provided with a cooler in which, after the ambient air is sucked in, the ambient air is then circulated in the closed cooling circuit and cooled by the cooler.
2.- The method according to aspect 1, wherein the method includes a step of measuring or determining a temperature in the vessel or at the outlet of the vessel after the vessel has been cooled with the first cooling cycle and, if the temperature is higher than a predetermined maximum temperature, additional cooling of this vessel with the second cooling cycle.
3.- The method according to aspect 1, wherein the method includes a step of determining or measuring a dew point at the outlet or determining or measuring an average dew point at the outlet over a predetermined period of time before the vessel is cooled, and:
- if this dew point is equal to or higher than a predetermined maximum dew point, cool this vessel with the second cooling cycle; and - if this dew point is lower than the predetermined maximum dew point, cool this vessel with the first cooling cycle.
Date Recue/Date Received 2023-08-11 4.- The method according to any one of aspects 1 to 3, wherein, for the second cooling cycle, the method also consists of using an expansion valve to expand the gas branched, dried, compressed at the outlet.
5.- The method according to any one of aspects Ito 4, wherein the method consists of providing a regeneration cycle to regenerate a vessel that is being regenerated, where this regeneration cycle consists of heating ambient air, passing it through the vessel in question and then blowing it off.
6.- A drying device for drying compressed gas, which the drying device is equipped with an inlet for compressed gas to be dried and an outlet for dried compressed gas, wherein the drying device comprises at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block which connect the aforementioned inlet, respectively the outlet, to the aforementioned vessels, the controllable valve system being such that at least one vessel will dry the compressed gas, while the other vessel is successively regenerated and cooled, wherein by regulation of the valve system, the vessels each in turn the dry compressed gas, whereby the drying device is additionally equipped with a blower to suck in ambient air, a gas release port and a four-way valve, valve block or similar which will allow either the blower or the gas release port to be connected to the vessels via the first valve block, in such a way that when the four-way valve connects the blower with the first valve block, the ambient air sucked in by the blower can enter the vessel to be cooled via the four-way valve and the first valve block, wherein the drying device is further equipped with a branch pipe which can branch off dried compressed gas, expand it and lead it via the second valve block to the vessel to be cooled, in such a way that, when the four-way valve connects the gas release port with the first valve block, the branched gas can be blown off via the gas release port after passing through the vessel to be cooled, wherein the drying device is further equipped with a cooling pipe connecting the second valve block with the inlet side of the blower in such a way that a closed cooling circuit is formed when the four-way Date Recue/Date Received 2023-08-11 valve, the valve block or such connects the blower to the first valve block which is a closed cooling circuit formed successively by the blower, the four way-valve, the first valve block, a vessel, the second valve block and the cooling pipe, wherein the cooling pipe is provided with a cooler.
7.- The drying device according to aspect 6, wherein the drying device is further equipped with a regeneration pipe which includes a heater, which regeneration pipe connects the four-way valve with the second valve block, wherein, when the four-way valve connects the gas release port with the first valve block, the four-way valve connects the blower to the regeneration pipe and thus to the second valve block in such a way that a regeneration circuit is formed comprising the blower, the four-way valve, the regeneration pipe with the heater, the second valve block, the vessel to be regenerated, the first valve block, the four-way valve and the gas release port.
8.- The drying device according to aspect 7, wherein the regeneration pipe and the cooling pipe partially coincide.
9.- The drying device according to any one of aspects 6 to 8, wherein the branching pipe contains an expansion valve.
10.- The drying device according to any one of aspects 6 to 9, wherein the branching pipe is integrated in, or part of, the second valve block.
Date Recue/Date Received 2023-08-11
[0104] Another aspect of the invention concerns a method for drying compressed gas by means of a drying device with an inlet for the compressed gas to be dried and an outlet for the dried compressed gas, comprising at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block connecting the aforementioned inlet, respectively outlet to the aforementioned vessels, wherein the controllable valve system is being regulated as such that at least one vessel will dry compressed gas, while the other vessel is successively regenerated and cooled, wherein by regulating the valve system the vessels dry each in turn compressed gas, characterized in that the method consists of providing a regeneration cycle to regenerate a vessel which is being regenerated, wherein this regeneration cycle consists of heating ambient air, passing it through the vessel concerned and then blowing it off.
[0105] This means applying the aforementioned regeneration cycle in a known drying device 1, i.e. without necessarily having to apply the first and second cooling cycles.
[0106] The present invention is by no means limited to the embodiments described as examples and shown in the figures, but a method and device according to the invention can be implemented in all shapes and sizes without going beyond the scope of the invention.
[0107] The following aspects are also disclosed herein:
1.- A method for drying compressed gas by means of a drying device with an inlet for compressed gas to be dried and an outlet for dried compressed gas, which drying device comprises at least two vessels filled with a Date Recue/Date Received 2023-08-11 regenerable desiccant and a controllable valve system, consisting of a first valve block and a second valve block connecting the above inlet, respectively outlet to the aforementioned vessels, the controllable valve system being regulated such that at least one vessel will dry compressed gas, while the other vessel will be regenerated and cooled successively, wherein, by regulating the valve system, the vessels each, in turn, dry compressed gas, whereby the method consists of providing a first cooling cycle and a second cooling cycle to cool the vessel being cooled, wherein the first cooling cycle consists of passing ambient air through the vessel and the second cooling cycle consisting of branching off dried compressed gas at the aforementioned outlet, expand it and pass it through the vessel to be cooled, after which this gas is then blown off, wherein depending on predetermined conditions, the first cooling cycle or the second cooling cycle, or both, will be applied, wherein the method also consists, for the first cooling cycle, of using a closed cooling circuit provided with a cooler in which, after the ambient air is sucked in, the ambient air is then circulated in the closed cooling circuit and cooled by the cooler.
2.- The method according to aspect 1, wherein the method includes a step of measuring or determining a temperature in the vessel or at the outlet of the vessel after the vessel has been cooled with the first cooling cycle and, if the temperature is higher than a predetermined maximum temperature, additional cooling of this vessel with the second cooling cycle.
3.- The method according to aspect 1, wherein the method includes a step of determining or measuring a dew point at the outlet or determining or measuring an average dew point at the outlet over a predetermined period of time before the vessel is cooled, and:
- if this dew point is equal to or higher than a predetermined maximum dew point, cool this vessel with the second cooling cycle; and - if this dew point is lower than the predetermined maximum dew point, cool this vessel with the first cooling cycle.
Date Recue/Date Received 2023-08-11 4.- The method according to any one of aspects 1 to 3, wherein, for the second cooling cycle, the method also consists of using an expansion valve to expand the gas branched, dried, compressed at the outlet.
5.- The method according to any one of aspects Ito 4, wherein the method consists of providing a regeneration cycle to regenerate a vessel that is being regenerated, where this regeneration cycle consists of heating ambient air, passing it through the vessel in question and then blowing it off.
6.- A drying device for drying compressed gas, which the drying device is equipped with an inlet for compressed gas to be dried and an outlet for dried compressed gas, wherein the drying device comprises at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block which connect the aforementioned inlet, respectively the outlet, to the aforementioned vessels, the controllable valve system being such that at least one vessel will dry the compressed gas, while the other vessel is successively regenerated and cooled, wherein by regulation of the valve system, the vessels each in turn the dry compressed gas, whereby the drying device is additionally equipped with a blower to suck in ambient air, a gas release port and a four-way valve, valve block or similar which will allow either the blower or the gas release port to be connected to the vessels via the first valve block, in such a way that when the four-way valve connects the blower with the first valve block, the ambient air sucked in by the blower can enter the vessel to be cooled via the four-way valve and the first valve block, wherein the drying device is further equipped with a branch pipe which can branch off dried compressed gas, expand it and lead it via the second valve block to the vessel to be cooled, in such a way that, when the four-way valve connects the gas release port with the first valve block, the branched gas can be blown off via the gas release port after passing through the vessel to be cooled, wherein the drying device is further equipped with a cooling pipe connecting the second valve block with the inlet side of the blower in such a way that a closed cooling circuit is formed when the four-way Date Recue/Date Received 2023-08-11 valve, the valve block or such connects the blower to the first valve block which is a closed cooling circuit formed successively by the blower, the four way-valve, the first valve block, a vessel, the second valve block and the cooling pipe, wherein the cooling pipe is provided with a cooler.
7.- The drying device according to aspect 6, wherein the drying device is further equipped with a regeneration pipe which includes a heater, which regeneration pipe connects the four-way valve with the second valve block, wherein, when the four-way valve connects the gas release port with the first valve block, the four-way valve connects the blower to the regeneration pipe and thus to the second valve block in such a way that a regeneration circuit is formed comprising the blower, the four-way valve, the regeneration pipe with the heater, the second valve block, the vessel to be regenerated, the first valve block, the four-way valve and the gas release port.
8.- The drying device according to aspect 7, wherein the regeneration pipe and the cooling pipe partially coincide.
9.- The drying device according to any one of aspects 6 to 8, wherein the branching pipe contains an expansion valve.
10.- The drying device according to any one of aspects 6 to 9, wherein the branching pipe is integrated in, or part of, the second valve block.
Date Recue/Date Received 2023-08-11
Claims (10)
1.- A method for drying compressed gas by means of a drying device with an inlet for compressed gas to be dried and an outlet for dried compressed gas, which drying device comprises at least two vessels filled with a regenerable desiccant and a controllable valve system, consisting of a first valve block and a second valve block connecting the above inlet, respectively outlet to the aforementioned vessels, the controllable valve system being regulated such that at least one vessel will dry compressed gas, while the other vessel will be regenerated and cooled successively, wherein, by regulating the valve system, the vessels each, in turn, dry compressed gas, whereby the method consists of providing a first cooling cycle and a second cooling cycle to cool the vessel being cooled, wherein the first cooling cycle consists of passing ambient air through the vessel and the second cooling cycle consisting of branching off dried compressed gas at the aforementioned outlet, expand it and pass it through the vessel to be cooled, after which this dried compressed gas is then blown off, wherein depending on predetermined conditions, the first cooling cycle or the second cooling cycle, or both, will be applied, wherein the method also consists, for the first cooling cycle, of using a closed cooling circuit provided with a cooler in which, after the ambient air is sucked in, the ambient air is then circulated in the closed cooling circuit and cooled by the cooler.
2.- The method according to claim 1, wherein the method includes a step of measuring or determining a temperature in the vessel or at the outlet of the vessel after the vessel has been cooled with the first cooling cycle and, if the temperature is higher than a predetermined maximum temperature, additional cooling of this vessel with the second cooling cycle.
3.- The method according to claim 1, wherein the method includes a step of determining or measuring a dew point at the outlet or determining or Date Recue/Date Received 2023-08-11 measuring an average dew point at the outlet over a predetermined period of time before the vessel is cooled, and:
- if this dew point is equal to or higher than a predetermined maximum dew point, cool this vessel with the second cooling cycle; and - if this dew point is lower than the predetermined maximum dew point, cool this vessel with the first cooling cycle.
- if this dew point is equal to or higher than a predetermined maximum dew point, cool this vessel with the second cooling cycle; and - if this dew point is lower than the predetermined maximum dew point, cool this vessel with the first cooling cycle.
4.- The method according to any one of claims 1 to 3, wherein, for the second cooling cycle, the method also consists of using an expansion valve to expand the gas branched, dried, compressed at the outlet.
5.- The method according to any one of claims 1 to 4, wherein the method consists of providing a regeneration cycle to regenerate a vessel that is being regenerated, where this regeneration cycle consists of heating ambient air, passing it through the vessel in question and then blowing it off.
6.- A drying device for drying compressed gas, which the drying device is equipped with an inlet for compressed gas to be dried and an outlet for dried compressed gas, wherein the drying device comprises at least two vessels filled with a regenerable desiccant and a controllable valve system consisting of a first valve block and a second valve block which connect the aforementioned inlet, respectively the outlet, to the aforementioned vessels, the controllable valve system being such that at least one vessel will dry the compressed gas, while the other vessel is successively regenerated and cooled, wherein by regulation of the valve system, the vessels each in turn the dry compressed gas, whereby the drying device is additionally equipped with a blower to suck in ambient air, a gas release port and a four-way valve, valve block or similar which will allow either the blower or the gas release port to be connected to the vessels via the first valve block, in such a way that when the four-way valve connects the blower with the first valve block, the ambient air sucked in by the blower can enter the vessel to be cooled via the four-way valve and the first valve block, wherein the drying device is further equipped Date Recue/Date Received 2023-08-11 with a branch pipe which can branch off dried compressed gas, expand it and lead it via the second valve block to the vessel to be cooled, in such a way that, when the four-way valve connects the gas release port with the first valve block, the branched gas can be blown off via the gas release port after passing through the vessel to be cooled, wherein the drying device is further equipped with a cooling pipe connecting the second valve block with the inlet side of the blower in such a way that a closed cooling circuit is formed when the four-way valve, the valve block or such connects the blower to the first valve block which is a closed cooling circuit formed successively by the blower, the four way-w valve, the first valve block, a vessel, the second valve block and the cooling pipe, wherein the cooling pipe is provided with a cooler.
7.- The drying device according to claim 6, wherein the drying device is further equipped with a regeneration pipe which includes a heater, which regeneration pipe connects the four-way valve with the second valve block, wherein, when the four-way valve connects the gas release port with the first valve block, the four-way valve connects the blower to the regeneration pipe and thus to the second valve block in such a way that a regeneration circuit is formed comprising the blower, the four-way valve, the regeneration pipe with the heater, the second valve block, the vessel to be regenerated, the first valve block, the four-way valve and the gas release port.
8.- The drying device according to claim 7, wherein the regeneration pipe and the cooling pipe partially coincide.
9.- The drying device according to any one of claims 6 to 8, wherein the branching pipe contains an expansion valve.
10.- The drying device according to any one of claims 6 to 9, wherein the branching pipe is integrated in, or part of, the second valve block.
Date Recue/Date Received 2023-08-11
Date Recue/Date Received 2023-08-11
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE2020/4999 | 2020-01-02 | ||
| BE20204999A BE1027958B1 (en) | 2020-01-02 | 2020-01-02 | Drying device and method for drying compressed gas |
| PCT/IB2020/062470 WO2021137126A1 (en) | 2020-01-02 | 2020-12-28 | Drying device and method for drying compressed gas |
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| BE1030642B1 (en) * | 2022-06-16 | 2024-01-22 | Atlas Copco Airpower Nv | Device for drying compressed gas and compressor installation provided with such device. |
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| GB1004741A (en) * | 1964-03-11 | 1965-09-15 | British Oxygen Co Ltd | Process for the purification of gases |
| SE7410521L (en) * | 1974-08-19 | 1976-02-20 | Alf Johan Hamrin | SET AND SYSTEM FOR CONTINUALLY REMOVING MOISTURE FROM A MEDIA CREAM, PREFERABLY COMPRESSOR AIR. |
| JPS6087830A (en) * | 1983-10-18 | 1985-05-17 | Daido Plant Kogyo Kk | Regenerating process of drying agent for dehumidifyer of compressed gas |
| JPS61204629U (en) * | 1985-06-12 | 1986-12-23 | ||
| DE3904791C1 (en) * | 1989-02-17 | 1990-07-26 | Zander Aufbereitungstechnik Gmbh, 4300 Essen, De | |
| BE1016309A3 (en) * | 2004-11-10 | 2006-07-04 | Atlas Copco Airpower Nv | METHOD FOR DRYING COMPRESSED GAS AND APPARATUS APPLIED THEREOF |
| CN100446842C (en) * | 2005-11-07 | 2008-12-31 | 韩国银河流体(空气)技术有限公司 | Apparatus for circulating regenerated air and drying compressed air by use of fan |
| CN201823451U (en) * | 2010-08-31 | 2011-05-11 | 杭州日盛净化设备有限公司 | Blast heating internal circulation compressed air purifying device |
| US9186623B2 (en) * | 2013-03-13 | 2015-11-17 | Roger's Machinery Company, Inc. | Recycled purge air dryer system and method of use |
| US9956521B2 (en) * | 2015-04-03 | 2018-05-01 | Ingersoll-Rand Company | Blower purge dryer with cooling apparatus and methodology |
| US9744496B1 (en) * | 2016-04-15 | 2017-08-29 | Beko Technologies Gmbh | Method for controlling an adsorption dryer for the treatment of compressed gas |
| CN206566718U (en) * | 2017-03-20 | 2017-10-20 | 杭州山立净化设备股份有限公司 | Compact Wind-cooling type air blast hot recycling absorption drier |
| KR101906531B1 (en) * | 2017-10-16 | 2018-12-18 | 에스피엑스플로우테크놀로지 주식회사 | Non-purge and adsorption type air dryer using a blower |
| CN108355466A (en) * | 2018-03-28 | 2018-08-03 | 珠海华信净化设备有限公司 | A kind of waste heat regenerating drier |
| CN109731444A (en) * | 2019-01-22 | 2019-05-10 | 无锡联合超滤净化设备科技有限公司 | A kind of regenerative system is unpowered zero gas consumption compression Technology of Thermal Drying and device |
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- 2020-12-28 FI FIEP20838298.6T patent/FI4084891T3/en active
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| KR20220111718A (en) | 2022-08-09 |
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| EP4084891A1 (en) | 2022-11-09 |
| JP2023507849A (en) | 2023-02-27 |
| BE1027958A1 (en) | 2021-07-29 |
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| AU2020418611A1 (en) | 2022-07-21 |
| BR112022010140A2 (en) | 2022-08-09 |
| US20230001345A1 (en) | 2023-01-05 |
| CN114929362A (en) | 2022-08-19 |
| EP4084891B1 (en) | 2023-11-22 |
| WO2021137126A1 (en) | 2021-07-08 |
| KR102696333B1 (en) | 2024-08-16 |
| CA3159257A1 (en) | 2021-07-08 |
| EP4324546A1 (en) | 2024-02-21 |
| JP7490780B2 (en) | 2024-05-27 |
| PL4084891T3 (en) | 2024-04-02 |
| AU2020418611B2 (en) | 2023-07-06 |
| CN114929362B (en) | 2024-04-26 |
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